Cell culture clarification
A method and a kit for cell culture clarification, as well as a system or apparatus for clarifying a cell culture and purifying biomolecules of interest, are described. The cell culture comprises at least one biomolecule of interest. The method comprises adding one or more compounds to the cell culture that allow the formation of floccules of solutes and/or particulates in said cell culture harvest, adding an amount of diatomaceous earth (DE) to said cell culture harvest, agitating the obtained solution, and transferring said solution to a filtration vessel comprising a support filter having a surface, whereby the diatomaceous earth in said solution forms a layer on said surface and filtering said harvest solution through said layer and support filter.
1. A method for cell culture clarification comprising:
(a) adding at least three compounds to a cell culture harvest comprising at least one of an IgG1 monoclonal antibody and an IgG4 monoclonal antibody, wherein the at least three compounds facilitate the formation of floccules of solutes and/or particulates in said cell culture harvest, and wherein said cell culture harvest resides in a bioreactor or in an intermediate vessel downstream of a bioreactor producing said cell culture harvest, wherein the at least three compounds are chosen from the group consisting of fatty acids having 7 to 10 carbon atoms and derivatives thereof, ureides, and electropositive compounds;
(b) adding an amount of diatomaceous earth (DE) to said cell culture harvest, wherein said added amount is from 20 to 60% of a measured cell culture wet cell weight;
(c) agitating said cell culture harvest to form a harvest solution;
(d) transferring the harvest solution to a filtration vessel comprising an inlet, an outlet, a reservoir and a support filter having a surface impermeable to DE and permitting said DE in said harvest solution to form a DE layer on said surface, wherein the harvest solution in the filtration vessel is not agitated;
(e) filtering said harvest solution in the filtration vessel through said layer and support filter at a flowrate of 400 to 2000 liters per square meter per hour; and
(f) collecting a clarified harvest from the outlet of the filtration vessel.
2. The method according to claim 1 , wherein a pressure differential allows the formation of said DE layer on said surface.
3. The method according to claim 1 , wherein in step (a) one or more of the fatty acids having 7 to 10 carbon atoms or derivatives thereof, one or more of the ureides which includes allantoin, and one or more of the electropositive compounds are added to the cell culture harvest.
4. The method according to claim 1 , wherein said diatomaceous earth is added directly to said bioreactor.
5. The method according to claim 1 , in which step (a) and (b) are simultaneous.
6. The method according to claim 1 , wherein said amount of DE is added prior to step (a).
7. The method according to claim 1 , wherein between 0.1% to 1.0% v/v of one or more of the fatty acids or derivatives thereof, between 0.5% to 3% w/v of one of more of the ureides including allantoin, and between 0.01% to 1% w/v of one or more of the electropositive compounds are added to the culture harvest.
8. The method according to claim 1 , wherein the electropositive compounds are one of the compounds added to the cell culture harvest and are selected from the group consisting of electropositive polysaccharide, electropositive polymer, chitosan, a chitosan derivative, a synthetic polymer, pDADMAC, a cationic surfactant and any combination thereof.
9. The method according to claim 1 , wherein said filtering step (e) comprises filtering the harvest solution at a flowrate of between 1000 and 2000 liters per square meter per hour.
10. The method according to claim 1 , wherein the electropositive compounds include chitosan having a molecular weight of from 30 kDa to 1000 kDa, and the chitosan is one of the compounds added to the cell culture harvest.
11. The method according to claim 10 , wherein the chitosan has a molecular weight of from 325 kDa to 375 kDa.
12. The method according to claim 1 , wherein the inlet of the filtration vessel is above the outlet of the filtration vessel, and the support filter is located proximate the outlet and below the inlet so that the DE layer can be formed by gravity or pumping.